US20070095087A1 - Vapor compression cooling system for cooling electronics - Google Patents
Vapor compression cooling system for cooling electronics Download PDFInfo
- Publication number
- US20070095087A1 US20070095087A1 US11/264,406 US26440605A US2007095087A1 US 20070095087 A1 US20070095087 A1 US 20070095087A1 US 26440605 A US26440605 A US 26440605A US 2007095087 A1 US2007095087 A1 US 2007095087A1
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- refrigerant
- quality
- microprocessor
- pressurized
- evaporator
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B40/00—Subcoolers, desuperheaters or superheaters
-
- G—PHYSICS
- G06—COMPUTING; CALCULATING OR COUNTING
- G06F—ELECTRIC DIGITAL DATA PROCESSING
- G06F1/00—Details not covered by groups G06F3/00 - G06F13/00 and G06F21/00
- G06F1/16—Constructional details or arrangements
- G06F1/20—Cooling means
-
- G—PHYSICS
- G06—COMPUTING; CALCULATING OR COUNTING
- G06F—ELECTRIC DIGITAL DATA PROCESSING
- G06F2200/00—Indexing scheme relating to G06F1/04 - G06F1/32
- G06F2200/20—Indexing scheme relating to G06F1/20
- G06F2200/201—Cooling arrangements using cooling fluid
Definitions
- This invention relates to cooling systems for electronics, and more particularly to vapor compression cooling systems for cooling at least one microprocessor.
- a vapor compression cooling system for cooling at least one microprocessor.
- the cooling system includes a compressor to pressurize a refrigerant used in the cooling system, a condenser to condense pressurized refrigerant received from the compressor, an expansion device to expand pressurized refrigerant received from the condenser, and a cold plate.
- the cold plate includes a surface that mates with a heat rejecting surface of a corresponding microprocessor, and an evaporator to receive expanded refrigerant from the expansion device, transfer heat from the corresponding microprocessor to the expanded refrigerant, and return heated refrigerant back to the system with a quality of less than 100%.
- the cooling system further includes a suction line heat exchanger to receive heated refrigerant from the evaporator at a quality of less than 100% and transfer heat from the pressurized refrigerant to the heated refrigerant to provide refrigerant at a quality of at least 100% back to the compressor.
- the suction line heat exchanger is located downstream from the condenser with respect to the refrigerant flow through the system to receive the pressurized refrigerant from the condenser.
- the suction line heat exchanger is located upstream from the condenser with respect to the refrigerant flow through the system to deliver the pressurized refrigerant to the condenser.
- the cooling system includes another cold plate including a surface that mates with a heat rejecting surface of a corresponding microprocessor and an evaporator to receive expanded refrigerant from the expansion device, transfer heat from the corresponding microprocessor to the expanded refrigerant, and return heated refrigerant back to the system with a quality of less than 100%.
- a method for operating a vapor compression cooling system to cool at least one microprocessor.
- the method includes the steps of compressing a refrigerant to provide pressurized refrigerant to the system, condensing the pressurized refrigerant to provide condensed refrigerant to the system, expanding the condensed refrigerant to provide cooled refrigerant to the system, transferring heat from a microprocessor to the cooled refrigerant to provide heated refrigerant with a quality of less than 100% to the system, and transferring additional heat from the pressurized refrigerant to the heated refrigerant to provide refrigerant with a quality of at least 100% to the system for use in the step of compressing.
- a method for operating a vapor compression cooling system to cool at least one microprocessor.
- the method includes the steps of compressing a refrigerant to provide pressurized refrigerant to the system, condensing the pressurized refrigerant to provide condensed refrigerant to the system, expanding the condensed refrigerant to provide cooled refrigerant to the system, transferring heat from a microprocessor to the cooled refrigerant to provide heated refrigerant with a quality of less than 100% to the system, and transferring additional heat from the condensed refrigerant to the heated refrigerant to provide refrigerant with a quality of at least 100% to the system for use in the step of compressing.
- FIG. 1 is a diagrammatic representation of a cooling system embodying the present invention
- FIG. 2 is a refrigerant pressure vs. enthalpy diagram representing operation of the system of FIG. 1 ;
- FIG. 3 is a diagrammatic representation of another vapor compression cooling system embodying the present invention.
- FIG. 4 is a refrigerant pressure vs. enthalpy diagram representing operation of the system of FIG. 3 .
- a vapor compression cooling system and method 10 are provided for cooling one or more microprocessors, such as the microprocessor shown schematically at 12 and the microprocessor shown schematically at 14 .
- the cooling system utilizes a suitable refrigerant, such as R 134 a , which is circulated through the cooling system via pressurization provided by a compressor 16 , which is preferably an electric motor driven compressor with speed control.
- the cooling system further includes a condenser 18 , an expansion device 20 , a pair of cold plates 22 and 24 , each associated with a corresponding one of the microprocessor 12 and 14 , and a suction line heat exchanger (SLHX) 26 .
- SSHX suction line heat exchanger
- Each of the cold plates 22 and 24 includes a surface 28 and 30 that mates with the corresponding microprocessor 12 and 14 , and an evaporator, shown schematically at 32 and 34 , that receives heat generated by the corresponding microprocessor 12 , 14 .
- One typical footprint for a microprocessor 12 or 14 would be a rectangular footprint with a width of 13 mm and a length of 9 mm, with a heat rejection of 175 watts.
- Quality is as conventionally defined, namely, the weight ratio % of the mass of refrigerant in the vapor phase to the total mass of the refrigerant, i.e., the combined mass of liquid refrigerant and vapor refrigerant, at a given point in the system.
- refrigerant wholly in the vapor phase will have a quality of 100%
- refrigerant wholly in the liquid phase will have a quality of 0%
- Refrigerant that is both in the liquid and vapor phase will have a quality greater than 0% and less than 100%, the exact number being determined by the ratio of refrigerant vapor to total refrigerant.
- the system 10 is designed to operate such that the quality of the refrigerant exiting the evaporator(s) 32 , 34 is less than 100% so as to maximize the cooling ability of the cold plate(s) 22 , 24 , i.e., to avoid dry-out of the evaporator(s) 32 , 34 .
- the suction line heat exchanger 26 is provided to protect the compressor 16 by increasing the quality of the refrigerant from the evaporator to at least 100% (and preferably in a superheated state) so as to provide vapor phase refrigerant to the compressor 16 .
- the phrase “a quality of at least 100%” is intended to mean that the refrigerant is at 100% quality or is in a superheated vapor state.
- the compressor 16 compresses the refrigerant to provide pressurized refrigerant to the system 10 , as shown schematically by the line 40 .
- the condenser 18 receives the pressurized refrigerant from the compressor 20 and transfers heat to a coolant flow 36 (preferably an air flow) so as to provide condensed refrigerant to the system, as shown schematically by the lines 42 .
- the expansion device 20 expands the condensed, pressurized refrigerant received from the condenser 18 to provide cooled refrigerant to the system, as shown schematically by the lines 44 .
- the cooled refrigerant is directed to the evaporator(s) 32 , 34 wherein heat is transferred from the microprocessor(s) 12 , 14 to the cooled refrigerant to provide heated refrigerant with a quality of less than 100% to the system, as shown schematically by the lines 46 .
- the heated refrigerant is directed to the suction line heat exchanger 26 wherein heat is transferred from the condensed refrigerant (which has also been directed to the suction line heat exchanger 26 downstream from the condenser 18 and upstream from the expansion device 20 ) to the heated refrigerant so as to provide refrigerant at 100% quality back to the compressor 16 , as shown schematically by the lines 48 .
- FIG. 2 The pressure and enthalpy of the refrigerant as it moves through the system is illustrated in FIG. 2 (assumes a ideal system) with the points A, A′; B, B′; C, C′: D, D′; E, E′; and F, F′ on the diagram corresponding to the like lettered locations in the system 10 of FIG. 1 .
- the refrigerant provided from the expansion device 20 to the evaporator(s) 32 , 34 could have an entrance quality of around 16.2% and the refrigerant provided from the evaporator(s) 32 , 34 to the system could have an exit quality of around 65%, with the refrigerant provided from the suction line heat exchanger 26 back to the compressor 16 having a super heat of approximately 5° C.
- the vapor compression cooling system 10 of FIG. 3 is similar to the system 10 of FIG. 1 with like numbers indicating like components, except for the location of the suction line heat exchanger 26 , which is shown located upstream of the condenser 18 in FIG. 3 rather than downstream from the condenser 18 such as in the system 10 of FIG. 1 .
- the system 10 of FIG. 3 is designed to operate such that the quality of the refrigerant exiting the evaporator(s) 32 , 34 is less than 100% so as to maximize the cooling ability of the cold plate(s) 22 , 24 , i.e., to avoid dry-out of the evaporator(s) 32 , 34 .
- the suction line heat exchanger 26 is provided to protect the compressor 16 by increasing the quality of the refrigerant from the evaporator to 100% so as to provide vapor phase refrigerant to the compressor 16 .
- the suction line heat exchanger 26 receives pressurized refrigerant from the compressor 16 , as shown schematically by the line 50 , and transfers heat from the pressurized refrigerant to the heated refrigerant received from the evaporator(s) 32 , 34 to provide refrigerant at 100% quality back to the compressor 16 , such as shown schematically by the line 52 .
- the pressurized refrigerant is then directed from the suction line heat exchanger 26 to the condenser 18 , such as shown schematically by the line 53 , so the condenser 18 can transfer heat from the pressurized refrigerant to a coolant flow 36 , such as an air flow, to provide condensed, pressurized refrigerant to the system 10 , such as shown schematically by the lines 54 .
- the expansion device 20 receives the condensed, pressurized refrigerant from the condenser 18 and expands the refrigerant to provide cooled refrigerant to the system 10 , such as shown schematically by the lines 36 .
- the expanded, cooled refrigerant is directed to the evaporator(s) 32 , 34 wherein heat is transferred from the microprocessor(s) 12 , 14 to the refrigerant to provide heated refrigerant back to the system with a quality of less than 100%, as shown schematically by the lines 58 .
- FIG. 4 is a pressure-enthalpy diagram for the refrigerant as it passes through the system 10 of FIG. 3 (assuming ideal system), with the letters A, A′; B, B′; C, C′; D, D′; E, E′; and F, F′ in the diagram of FIG. 4 corresponding to the like lettered locations in the system 10 of FIG. 3 .
- the refrigerant provided from the expansion device 20 to the evaporator(s) 32 , 34 could have an entrance quality of around 34.1% and the refrigerant provided from the evaporator(s) 32 , 34 to the system could have an exit quality of around 65%, with the refrigerant provided from the suction line heat exchanger 26 back to the compressor 16 having a super heat of approximately 5° C.
- the speed of the compressor is controlled via the speed of an electric compressor drive motor (not shown) using any suitable motor speed control in response to selected system parameters that are monitored using suitable sensors or probes (not shown).
- the exit temperatures of the refrigerant at points A and D in FIGS. 1 and 2 , and points A and C in FIGS. 3 and 4 could be monitored and compared to suitable set points that would yield the desired exit quality from the evaporator(s) 32 , 34 , with the speed of the compressor being increased or decreased to maintain the monitored temperatures within a suitable range of the set points.
- a temperature sensor 60 could be used to sense the exit temperature from the low pressure side of the suction line heat exchanger 26 with the sensed temperature then being used to control a thermal expansion valve, when the expansion device 20 is provided in that form.
- the suction line heat exchanger 26 it may be desirable for the suction line heat exchanger 26 to include a liquid accumulation function.
- FIGS. 1-4 have been shown herein as having two cold plates 22 and 24 , each cooling a corresponding one of the microprocessors 12 and 14 , it should be understood that the systems 10 could be configured with only a single cold plate or more than two cold plates, and that any given cold plate could be dedicated to cooling a single microprocessor or multiple microprocessors.
- the system 10 can provide optimal cooling of the microprocessor(s) 12 , 14 while protecting the compressor 16 from damage by providing refrigerant to the compressor with a quality of 100%.
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- Theoretical Computer Science (AREA)
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- General Physics & Mathematics (AREA)
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- Cooling Or The Like Of Electrical Apparatus (AREA)
- Cooling Or The Like Of Semiconductors Or Solid State Devices (AREA)
Abstract
Description
- This invention relates to cooling systems for electronics, and more particularly to vapor compression cooling systems for cooling at least one microprocessor.
- There is currently an ever-increasing demand to improve the processing speed, power, and memory of electronic devices, such as desktop computers, laptop or portable computers, hand-held computers, cellular phones, and such, while decreasing the overall size and weight of such devices. To this end, more powerful microprocessors are constantly being developed in smaller and smaller packages, but with increasing demands for heat rejection to remove the heat generated from the increased processing power and speed. To overcome challanges associated with heat rejection, a number of active cooling systems have been proposed for cooling microprocessors, and while many of these systems may prove adequate for this intended use, there is always room for improvement.
- According to one feature of the invention, a vapor compression cooling system is provided for cooling at least one microprocessor. The cooling system includes a compressor to pressurize a refrigerant used in the cooling system, a condenser to condense pressurized refrigerant received from the compressor, an expansion device to expand pressurized refrigerant received from the condenser, and a cold plate. The cold plate includes a surface that mates with a heat rejecting surface of a corresponding microprocessor, and an evaporator to receive expanded refrigerant from the expansion device, transfer heat from the corresponding microprocessor to the expanded refrigerant, and return heated refrigerant back to the system with a quality of less than 100%. The cooling system further includes a suction line heat exchanger to receive heated refrigerant from the evaporator at a quality of less than 100% and transfer heat from the pressurized refrigerant to the heated refrigerant to provide refrigerant at a quality of at least 100% back to the compressor.
- According to one feature, the suction line heat exchanger is located downstream from the condenser with respect to the refrigerant flow through the system to receive the pressurized refrigerant from the condenser.
- In one feature, the suction line heat exchanger is located upstream from the condenser with respect to the refrigerant flow through the system to deliver the pressurized refrigerant to the condenser.
- In accordance with one feature, the cooling system includes another cold plate including a surface that mates with a heat rejecting surface of a corresponding microprocessor and an evaporator to receive expanded refrigerant from the expansion device, transfer heat from the corresponding microprocessor to the expanded refrigerant, and return heated refrigerant back to the system with a quality of less than 100%.
- According to one feature of the invention, a method is provided for operating a vapor compression cooling system to cool at least one microprocessor. The method includes the steps of compressing a refrigerant to provide pressurized refrigerant to the system, condensing the pressurized refrigerant to provide condensed refrigerant to the system, expanding the condensed refrigerant to provide cooled refrigerant to the system, transferring heat from a microprocessor to the cooled refrigerant to provide heated refrigerant with a quality of less than 100% to the system, and transferring additional heat from the pressurized refrigerant to the heated refrigerant to provide refrigerant with a quality of at least 100% to the system for use in the step of compressing.
- In accordance with one feature of the invention, a method is provided for operating a vapor compression cooling system to cool at least one microprocessor. The method includes the steps of compressing a refrigerant to provide pressurized refrigerant to the system, condensing the pressurized refrigerant to provide condensed refrigerant to the system, expanding the condensed refrigerant to provide cooled refrigerant to the system, transferring heat from a microprocessor to the cooled refrigerant to provide heated refrigerant with a quality of less than 100% to the system, and transferring additional heat from the condensed refrigerant to the heated refrigerant to provide refrigerant with a quality of at least 100% to the system for use in the step of compressing.
- Other objects, features, and advantages of the invention will become apparent from a review of the entire specification, including the appended claims and drawings.
-
FIG. 1 is a diagrammatic representation of a cooling system embodying the present invention; -
FIG. 2 is a refrigerant pressure vs. enthalpy diagram representing operation of the system ofFIG. 1 ; -
FIG. 3 is a diagrammatic representation of another vapor compression cooling system embodying the present invention; and -
FIG. 4 is a refrigerant pressure vs. enthalpy diagram representing operation of the system ofFIG. 3 . - With reference to
FIG. 1 , a vapor compression cooling system andmethod 10 are provided for cooling one or more microprocessors, such as the microprocessor shown schematically at 12 and the microprocessor shown schematically at 14. The cooling system utilizes a suitable refrigerant, such as R134 a, which is circulated through the cooling system via pressurization provided by acompressor 16, which is preferably an electric motor driven compressor with speed control. The cooling system further includes acondenser 18, anexpansion device 20, a pair ofcold plates microprocessor cold plates corresponding microprocessor corresponding microprocessor microprocessor system 10 must be correctly sized for the required cooling of one or more of themicroprocessors cooling system 10 is used. Accordingly, further details of the precise construction and/or form of each of the components will not be given herein. - Reference herein will be made to the “quality of the refrigerant” or just the “quality”. Quality is as conventionally defined, namely, the weight ratio % of the mass of refrigerant in the vapor phase to the total mass of the refrigerant, i.e., the combined mass of liquid refrigerant and vapor refrigerant, at a given point in the system. Thus, refrigerant wholly in the vapor phase will have a quality of 100%, while refrigerant wholly in the liquid phase will have a quality of 0%. Refrigerant that is both in the liquid and vapor phase will have a quality greater than 0% and less than 100%, the exact number being determined by the ratio of refrigerant vapor to total refrigerant.
- The
system 10 is designed to operate such that the quality of the refrigerant exiting the evaporator(s) 32, 34 is less than 100% so as to maximize the cooling ability of the cold plate(s) 22,24, i.e., to avoid dry-out of the evaporator(s) 32,34. The suctionline heat exchanger 26 is provided to protect thecompressor 16 by increasing the quality of the refrigerant from the evaporator to at least 100% (and preferably in a superheated state) so as to provide vapor phase refrigerant to thecompressor 16. As used herein, the phrase “a quality of at least 100%” is intended to mean that the refrigerant is at 100% quality or is in a superheated vapor state. - In operation, the
compressor 16 compresses the refrigerant to provide pressurized refrigerant to thesystem 10, as shown schematically by theline 40. Thecondenser 18 receives the pressurized refrigerant from thecompressor 20 and transfers heat to a coolant flow 36 (preferably an air flow) so as to provide condensed refrigerant to the system, as shown schematically by thelines 42. Theexpansion device 20 expands the condensed, pressurized refrigerant received from thecondenser 18 to provide cooled refrigerant to the system, as shown schematically by thelines 44. The cooled refrigerant is directed to the evaporator(s) 32,34 wherein heat is transferred from the microprocessor(s) 12,14 to the cooled refrigerant to provide heated refrigerant with a quality of less than 100% to the system, as shown schematically by thelines 46. The heated refrigerant is directed to the suctionline heat exchanger 26 wherein heat is transferred from the condensed refrigerant (which has also been directed to the suctionline heat exchanger 26 downstream from thecondenser 18 and upstream from the expansion device 20) to the heated refrigerant so as to provide refrigerant at 100% quality back to thecompressor 16, as shown schematically by thelines 48. - The pressure and enthalpy of the refrigerant as it moves through the system is illustrated in
FIG. 2 (assumes a ideal system) with the points A, A′; B, B′; C, C′: D, D′; E, E′; and F, F′ on the diagram corresponding to the like lettered locations in thesystem 10 ofFIG. 1 . - As a working example of the
system 10 ofFIGS. 1 and 2 , the refrigerant provided from theexpansion device 20 to the evaporator(s) 32,34 could have an entrance quality of around 16.2% and the refrigerant provided from the evaporator(s) 32,34 to the system could have an exit quality of around 65%, with the refrigerant provided from the suctionline heat exchanger 26 back to thecompressor 16 having a super heat of approximately 5° C. - The vapor
compression cooling system 10 ofFIG. 3 is similar to thesystem 10 ofFIG. 1 with like numbers indicating like components, except for the location of the suctionline heat exchanger 26, which is shown located upstream of thecondenser 18 inFIG. 3 rather than downstream from thecondenser 18 such as in thesystem 10 ofFIG. 1 . As with thesystem 10 ofFIG. 1 , thesystem 10 ofFIG. 3 is designed to operate such that the quality of the refrigerant exiting the evaporator(s) 32, 34 is less than 100% so as to maximize the cooling ability of the cold plate(s) 22,24, i.e., to avoid dry-out of the evaporator(s) 32,34. The suctionline heat exchanger 26 is provided to protect thecompressor 16 by increasing the quality of the refrigerant from the evaporator to 100% so as to provide vapor phase refrigerant to thecompressor 16. - Accordingly, for the
system 10 ofFIG. 3 , the suctionline heat exchanger 26 receives pressurized refrigerant from thecompressor 16, as shown schematically by theline 50, and transfers heat from the pressurized refrigerant to the heated refrigerant received from the evaporator(s) 32,34 to provide refrigerant at 100% quality back to thecompressor 16, such as shown schematically by theline 52. The pressurized refrigerant is then directed from the suctionline heat exchanger 26 to thecondenser 18, such as shown schematically by theline 53, so thecondenser 18 can transfer heat from the pressurized refrigerant to acoolant flow 36, such as an air flow, to provide condensed, pressurized refrigerant to thesystem 10, such as shown schematically by thelines 54. Theexpansion device 20 receives the condensed, pressurized refrigerant from thecondenser 18 and expands the refrigerant to provide cooled refrigerant to thesystem 10, such as shown schematically by thelines 36. The expanded, cooled refrigerant is directed to the evaporator(s) 32,34 wherein heat is transferred from the microprocessor(s) 12,14 to the refrigerant to provide heated refrigerant back to the system with a quality of less than 100%, as shown schematically by thelines 58. - Again,
FIG. 4 is a pressure-enthalpy diagram for the refrigerant as it passes through thesystem 10 ofFIG. 3 (assuming ideal system), with the letters A, A′; B, B′; C, C′; D, D′; E, E′; and F, F′ in the diagram ofFIG. 4 corresponding to the like lettered locations in thesystem 10 ofFIG. 3 . - As a working example of the
system 10 ofFIGS. 3 and 4 , the refrigerant provided from theexpansion device 20 to the evaporator(s) 32,34 could have an entrance quality of around 34.1% and the refrigerant provided from the evaporator(s) 32,34 to the system could have an exit quality of around 65%, with the refrigerant provided from the suctionline heat exchanger 26 back to thecompressor 16 having a super heat of approximately 5° C. - While there are many possible control schemes that could be utilized in the
systems 10 ofFIGS. 1-4 to insure that the exit quality from the evaporator(s) 32,34 is less than 100%, in one preferred form, the speed of the compressor is controlled via the speed of an electric compressor drive motor (not shown) using any suitable motor speed control in response to selected system parameters that are monitored using suitable sensors or probes (not shown). For example, the exit temperatures of the refrigerant at points A and D inFIGS. 1 and 2 , and points A and C inFIGS. 3 and 4 could be monitored and compared to suitable set points that would yield the desired exit quality from the evaporator(s) 32,34, with the speed of the compressor being increased or decreased to maintain the monitored temperatures within a suitable range of the set points. By way of another example, a temperature sensor 60 could be used to sense the exit temperature from the low pressure side of the suctionline heat exchanger 26 with the sensed temperature then being used to control a thermal expansion valve, when theexpansion device 20 is provided in that form. In such a system, it may be preferred to include a receiver in the high pressure flow path between thecondenser 36 and the suctionline heat exchanger 26, with the potential for this receiver to be an integrated portion of thecondenser 36. As yet another example, when theexpansion device 20 is provided in the form of a fixed orifice, it may be desirable for the suctionline heat exchanger 26 to include a liquid accumulation function. - While the
systems 10 ofFIGS. 1-4 have been shown herein as having twocold plates microprocessors systems 10 could be configured with only a single cold plate or more than two cold plates, and that any given cold plate could be dedicated to cooling a single microprocessor or multiple microprocessors. - It should be appreciated that by providing a suction
line heat exchanger 26 in a vaporcompression cooling system 10 wherein the exit quality from the evaporator(s) 32,34 of the cooling plate(s) 22,24 is always maintained at less than 100%, thesystem 10 can provide optimal cooling of the microprocessor(s) 12,14 while protecting thecompressor 16 from damage by providing refrigerant to the compressor with a quality of 100%.
Claims (8)
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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US11/264,406 US20070095087A1 (en) | 2005-11-01 | 2005-11-01 | Vapor compression cooling system for cooling electronics |
DE102006050211A DE102006050211A1 (en) | 2005-11-01 | 2006-10-25 | Dampfkompresssionskühlsystem |
JP2006296295A JP2007150284A (en) | 2005-11-01 | 2006-10-31 | Steam pressure cooling system for cooling electronic apparatus |
Applications Claiming Priority (1)
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US11/264,406 US20070095087A1 (en) | 2005-11-01 | 2005-11-01 | Vapor compression cooling system for cooling electronics |
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US20070095087A1 true US20070095087A1 (en) | 2007-05-03 |
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US11/264,406 Abandoned US20070095087A1 (en) | 2005-11-01 | 2005-11-01 | Vapor compression cooling system for cooling electronics |
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US (1) | US20070095087A1 (en) |
JP (1) | JP2007150284A (en) |
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Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20080186679A1 (en) * | 2007-02-06 | 2008-08-07 | Hitoshi Matsushima | Disk array system and electronic apparatus |
US20080314064A1 (en) * | 2007-04-13 | 2008-12-25 | Al-Eidan Abdullah A | Air conditioning system |
US20100032150A1 (en) * | 2008-08-05 | 2010-02-11 | Pipeline Micro, Inc. | Microscale cooling apparatus and method |
CN102530803A (en) * | 2012-01-12 | 2012-07-04 | 苏权兴 | Refrigerant subpackage equipment |
US8291719B2 (en) * | 2007-10-09 | 2012-10-23 | Be Aerospace, Inc. | Thermal control system and method |
US20120279684A1 (en) * | 2010-07-13 | 2012-11-08 | Earl Keisling | Systems and methods for cooling electronic equipment |
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US20140116083A1 (en) * | 2012-10-29 | 2014-05-01 | Myungjin Chung | Refrigerator |
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US9234685B2 (en) * | 2012-08-01 | 2016-01-12 | Thermo King Corporation | Methods and systems to increase evaporator capacity |
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US10088238B2 (en) | 2011-06-27 | 2018-10-02 | Wisconsin Alumni Research Foundation | High efficiency thermal management system |
SE2050095A1 (en) * | 2020-01-30 | 2021-07-31 | Swep Int Ab | A refrigeration system |
US11384989B2 (en) | 2016-08-26 | 2022-07-12 | Inertech Ip Llc | Cooling systems and methods using single-phase fluid |
WO2022272116A1 (en) * | 2021-06-24 | 2022-12-29 | Booz Allen Hamilton Inc. | Thermal management systems |
Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5426952A (en) * | 1994-03-03 | 1995-06-27 | General Electric Company | Refrigerant flow rate control based on evaporator exit dryness |
US6351950B1 (en) * | 1997-09-05 | 2002-03-05 | Fisher & Paykel Limited | Refrigeration system with variable sub-cooling |
US6427454B1 (en) * | 2000-02-05 | 2002-08-06 | Michael K. West | Air conditioner and controller for active dehumidification while using ambient air to prevent overcooling |
US6467295B2 (en) * | 2000-12-01 | 2002-10-22 | Lg Electronics Inc. | Refrigerated cooling apparatus for semiconductor device |
US6490877B2 (en) * | 2001-03-09 | 2002-12-10 | Hewlett-Packard Company | Multi-load refrigeration system with multiple parallel evaporators |
US6543246B2 (en) * | 2001-07-24 | 2003-04-08 | Kryotech, Inc. | Integrated circuit cooling apparatus |
US6606867B1 (en) * | 2000-11-15 | 2003-08-19 | Carrier Corporation | Suction line heat exchanger storage tank for transcritical cycles |
US6679081B2 (en) * | 2000-04-04 | 2004-01-20 | Thermal Form & Function, Llc | Pumped liquid cooling system using a phase change refrigerant |
US20060016214A1 (en) * | 2004-07-14 | 2006-01-26 | Carrier Corporation | Refrigeration system |
US7007506B2 (en) * | 2000-03-09 | 2006-03-07 | Fujitsu Limited | Refrigeration system utilizing incomplete evaporation of refrigerant in evaporator |
US7017358B2 (en) * | 2003-03-19 | 2006-03-28 | Delta Design, Inc. | Apparatus and method for controlling the temperature of an electronic device |
US7055341B2 (en) * | 2000-12-04 | 2006-06-06 | Fujitsu Limited | High efficiency cooling system and heat absorbing unit |
US7111472B1 (en) * | 1996-04-04 | 2006-09-26 | Tube Ice, Llc | Circuit apparatus and configurations for refrigeration systems |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5749237A (en) * | 1993-09-28 | 1998-05-12 | Jdm, Ltd. | Refrigerant system flash gas suppressor with variable speed drive |
US6205803B1 (en) * | 1996-04-26 | 2001-03-27 | Mainstream Engineering Corporation | Compact avionics-pod-cooling unit thermal control method and apparatus |
-
2005
- 2005-11-01 US US11/264,406 patent/US20070095087A1/en not_active Abandoned
-
2006
- 2006-10-25 DE DE102006050211A patent/DE102006050211A1/en not_active Withdrawn
- 2006-10-31 JP JP2006296295A patent/JP2007150284A/en active Pending
Patent Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5426952A (en) * | 1994-03-03 | 1995-06-27 | General Electric Company | Refrigerant flow rate control based on evaporator exit dryness |
US7111472B1 (en) * | 1996-04-04 | 2006-09-26 | Tube Ice, Llc | Circuit apparatus and configurations for refrigeration systems |
US6351950B1 (en) * | 1997-09-05 | 2002-03-05 | Fisher & Paykel Limited | Refrigeration system with variable sub-cooling |
US6427454B1 (en) * | 2000-02-05 | 2002-08-06 | Michael K. West | Air conditioner and controller for active dehumidification while using ambient air to prevent overcooling |
US7007506B2 (en) * | 2000-03-09 | 2006-03-07 | Fujitsu Limited | Refrigeration system utilizing incomplete evaporation of refrigerant in evaporator |
US6679081B2 (en) * | 2000-04-04 | 2004-01-20 | Thermal Form & Function, Llc | Pumped liquid cooling system using a phase change refrigerant |
US6606867B1 (en) * | 2000-11-15 | 2003-08-19 | Carrier Corporation | Suction line heat exchanger storage tank for transcritical cycles |
US6467295B2 (en) * | 2000-12-01 | 2002-10-22 | Lg Electronics Inc. | Refrigerated cooling apparatus for semiconductor device |
US7055341B2 (en) * | 2000-12-04 | 2006-06-06 | Fujitsu Limited | High efficiency cooling system and heat absorbing unit |
US6490877B2 (en) * | 2001-03-09 | 2002-12-10 | Hewlett-Packard Company | Multi-load refrigeration system with multiple parallel evaporators |
US6543246B2 (en) * | 2001-07-24 | 2003-04-08 | Kryotech, Inc. | Integrated circuit cooling apparatus |
US7017358B2 (en) * | 2003-03-19 | 2006-03-28 | Delta Design, Inc. | Apparatus and method for controlling the temperature of an electronic device |
US20060016214A1 (en) * | 2004-07-14 | 2006-01-26 | Carrier Corporation | Refrigeration system |
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US20080314064A1 (en) * | 2007-04-13 | 2008-12-25 | Al-Eidan Abdullah A | Air conditioning system |
US8359882B2 (en) * | 2007-04-13 | 2013-01-29 | Al-Eidan Abdullah A | Air conditioning system with selective regenerative thermal energy feedback control |
US8689575B2 (en) | 2007-10-09 | 2014-04-08 | B/E Aerospace, Inc. | Thermal control system and method |
US8291719B2 (en) * | 2007-10-09 | 2012-10-23 | Be Aerospace, Inc. | Thermal control system and method |
US20100032150A1 (en) * | 2008-08-05 | 2010-02-11 | Pipeline Micro, Inc. | Microscale cooling apparatus and method |
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EP2593845A4 (en) * | 2010-07-13 | 2015-04-22 | Inertech Ip Llc | Systems and methods for cooling electronic equipment |
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US20120279684A1 (en) * | 2010-07-13 | 2012-11-08 | Earl Keisling | Systems and methods for cooling electronic equipment |
US9212834B2 (en) * | 2011-06-17 | 2015-12-15 | Greener-Ice Spv, L.L.C. | System and method for liquid-suction heat exchange thermal energy storage |
US20130145780A1 (en) * | 2011-06-17 | 2013-06-13 | Ice Energy, Inc. | System and method for liquid-suction heat exchange thermal energy storage |
US10088238B2 (en) | 2011-06-27 | 2018-10-02 | Wisconsin Alumni Research Foundation | High efficiency thermal management system |
US9625182B2 (en) * | 2011-12-20 | 2017-04-18 | Aairbus Defence And Space Sas | Cooling device |
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US9234685B2 (en) * | 2012-08-01 | 2016-01-12 | Thermo King Corporation | Methods and systems to increase evaporator capacity |
US20140102682A1 (en) * | 2012-10-16 | 2014-04-17 | Doowon Climate Control Co., Ltd. | Condenser for vehicle |
US20140116083A1 (en) * | 2012-10-29 | 2014-05-01 | Myungjin Chung | Refrigerator |
US20170082334A1 (en) * | 2014-05-30 | 2017-03-23 | Mitsubishi Electric Corporation | Air-conditioning apparatus |
US10451324B2 (en) * | 2014-05-30 | 2019-10-22 | Mitsubishi Electric Corporation | Air-conditioning apparatus |
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US20160223239A1 (en) * | 2015-01-31 | 2016-08-04 | Trane International Inc. | Indoor Liquid/Suction Heat Exchanger |
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DE102006050211A1 (en) | 2007-08-02 |
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